Measuring transducer of vibration-type

Abstract

A measuring transducer includes a transducer housing, as well as an internal part arranged in the transducer housing. The internal part includes at least one curved measuring tube vibrating, at least at times, during operation and serving for conveying the medium, as well as a counteroscillator affixed to the measuring tube on the inlet-side, accompanied by formation of a coupling zone, and to the measuring tube on the outlet-side, accompanied by the formation of a coupling zone. The internal part is held oscillatably in the transducer housing, at least by means of two connecting tube pieces, via which the measuring tube communicates during operation with the pipeline and which are so oriented with respect to one another, as well as with respect to an imaginary longitudinal axis of the measuring transducer, that the internal part can move during operation in the manner of a pendulum about the longitudinal axis. The measuring tube and the counteroscillator are additionally so embodied and so oriented with respect to one another that both a center of mass spaced from the imaginary longitudinal axis of the measuring tube, as well as also a center of mass of the counteroscillator spaced from the imaginary longitudinal axis, lie in a common region of the measuring transducer spanned by the imaginary longitudinal axis and the measuring tube, and that the center of mass of the measuring tube is spaced farther from the longitudinal axis than the center of mass of the counteroscillator.

Description

[0001]This application is a nonprovisional of U.S. Provisional Application 60 / 752,372 filed on Dec. 22, 2005 and U.S. Provisional Application 60 / 752,374 filed on Dec. 22, 2005 and which claims the benefit of German application numbers 102005062007.8 filed on Dec. 22, 2005 and 102005062004.3 filed on Dec. 22, 2005.FIELD OF THE INVENTION[0002]The invention relates to a measuring transducer of vibration-type, especially one for use in a Coriolis mass flow meter.BACKGROUND OF THE INVENTION[0003]For determining a mass flow of a medium flowing in a pipeline, especially a liquid or other fluid, often such measuring devices are used which, by means of a measuring transducer of vibration-type and a control and evaluation electronics connected thereto, effect in the fluid Coriolis forces and, derived from these forces, produce a measurement signal representing mass flow. Such measuring transducers, especially also their use in Coriolis mass flow meters, have been known already for a long time...

AI Technical Summary

Benefits of technology

The invention is about improving the density dependence of measuring transducers of this kind by making the zero point and stability better. This is achieved by designing the measuring tube and counteroscillator in a way that they can both move dynamically in the pipeline. The internal part of the measuring tube vibrates, and the counteroscillator forms two coupling zones that move in a way that compensates for the internal part's movement. This allows the measuring tube to have a well-balanced response over a wide range of densities. The invention also includes various ways to orient the measuring tube and counteroscillator with respect to the pipeline and the transducer's housing. The goal is to make the measuring transducer more robust and effective in measuring the medium flow in a pipeline.

Problems solved by technology

Consequently, for this case, measuring tubes are preferably of titanium or zirconium, which are, however, on the basis of the higher cost of material and the usually also higher processing expense, much more expensive than those of stainless steel.

Such distributor pieces are on the one hand complicated to manufacture and on the other hand also represent flow bodies having a marked inclination for the formation of accretions or for plugging.

Due to the mostly rather narrow band width of counteroscillators in the wanted mode, measuring transducers with a single curved measuring tube have, however, often for applications where density of the medium fluctuates over a wide range, especially also in comparison to such measuring transducers with two parallel measuring tubes, the disadvantage that, as a result of the imbalance of the internal part fluctuating with the density, the zero point of the measuring transducer and consequently also the measuring accuracy of the respective inline measuring device can equally fluctuate significantly and as, a result, can be correspondingly decreased.

This is a result of, among other things, that also by means of the usually single counteroscillator, transverse forces can only be incompletely neutralized and, therefore, only incompletely kept away from the connected pipeline.

These lateral oscillations of the internal part produce, correspondingly, also an additional elastic deformation of the connecting tube piece and can in this way effect also undesirable vibrations in the connected pipeline.

These are very similar to the Coriolis mode and, in any event, however, of equal frequency and consequently practically indistinguishable from the Coriolis mode, which, in turn, would make the measuring signal representing the actual mass flow unusable.

Unfortunately, in this case, however, the mass of the counteroscillator required for achieving a sufficiently robust damping of the transverse forces rises more than proportionately with the nominal diameter of the measuring tube.

This represents a great disadvantage for such measuring tubes of high nominal diameter, since a use of such components of high mass means, namely, always an increased cost of assembly, both in the manufacture, as well as also in the case of the installing of the measuring device into the pipeline.

Moreover, in this case, it is only possible to assure, at great complexity, that the smallest eigenfrequency of the measuring transducer which, yes, also does become always lower with increasing mass, lies, after as before, very far from the likewise low eigenfrequencies of the connected pipeline.

Consequently, a use of such a measuring transducer in industrially usable, inline measuring devices of the described kind, for example, Coriolis mass flow measuring devices, has long been rather limited to relatively low measuring-tube nominal diameters up to about 10 mm.

However, investigations have in the meantime shown that the zero point of measuring transducers of the named kind can be subject, at very low mass flow rates and media deviating as to density considerably from the calibrated reference density, after, as before, to considerable fluctuations.

Experimental investigations on measuring transducers configured according to U.S. Pat. No. 6,666,098, for which, as proposed, a relatively heavy counteroscillator has been used, have, it is true, led to the recognition that, in this way, there is quite a certain improvement of the null point stability and, as a result, an improvement of the measuring accuracy of inline measuring devices of the described kind, but, however, this has been achieved only to an unsatisfactory degree.

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